skip to main content
Guest
e-Shelf
My Account
Sign out
Sign in
This feature requires javascript
Tags
e-Journals
e-Books
Databases
USP Libraries
Help
Help
Language:
English
Spanish
Portuguese (Brazil)
This feature required javascript
This feature requires javascript
Primo Search
General Search
General Search
Physical Collection
Physical Collections
USP Intelectual Production
USP Production
Search For:
Clear Search Box
Search in:
General Search
Or select another collection:
Search in:
General Search
Advanced Search
Browse Search
This feature requires javascript
This feature requires javascript
Ammonia decomposition in the thermochemical waste-heat recuperation systems: A view from low and high heating value
Pashchenko, Dmitry ; Mustafin, Ravil
Energy conversion and management, 2022-01, Vol.251, p.114959, Article 114959
[Peer Reviewed Journal]
Oxford: Elsevier Ltd
Full text available
Citations
Cited by
View Online
Details
Reviews & Tags
More
Times Cited
This feature requires javascript
Actions
Add to e-Shelf
Remove from e-Shelf
E-mail
Print
Permalink
Citation
EasyBib
EndNote
RefWorks
Delicious
Export RIS
Export BibTeX
This feature requires javascript
Title:
Ammonia decomposition in the thermochemical waste-heat recuperation systems: A view from low and high heating value
Author:
Pashchenko, Dmitry
;
Mustafin, Ravil
Subjects:
Ammonia
;
Calorific value
;
Condensates
;
Decomposition
;
Decomposition reactions
;
Flue gas
;
Heat
;
Heat balance
;
Heat recovery
;
Heating equipment
;
Hydrogen-rich fuel
;
Mathematical analysis
;
Reactors
;
Steam
;
Thermochemical recuperation
;
Thermodynamic analysis
Is Part Of:
Energy conversion and management, 2022-01, Vol.251, p.114959, Article 114959
Description:
[Display omitted] •Thermochemical waste-heat recuperation by ammonia decomposition.•The maximum heat recovery rate is 0.83 in the temperature range of 500–500 °C.•13% of steam from exhaust gas has to be condensed to compensate heat deficit.•Heat recuperated in a reactor is 2–5 times higher than heat recuperated in a preheater.•The maximum heat transformation coefficient is 1.16. This paper is devoted to the investigation of the thermochemical waste-heat recuperation system based on ammonia decomposition. Thermochemical waste-heat recuperation system consists of a reactor, an ammonia preheater, and a condenser. The thermodynamic analysis of the TCR system was performed via Aspen HYSYS software. The heat balance was calculated for the different operating parameters such as temperature (100–700°C) and pressure (1–20 bar). The heat balance showed that in the temperature range from 150–500°C there are heat deficits in the TCR system. To cover this deficit up to 15% of steam from flue gas have to be condensed. For compensating the heat deficit was suggested using a condenser after a preheater. The heat of H2O condensation is covered a significant part of the heat deficit. The heat recovery rate was determined and showed that the TCR system has a maximum efficiency in the temperature range above 500°C and pressure above 20 bar. The heat recuperated in the reactor is 2–5 times higher than the heat recuperated in the preheater. The heat transformation coefficient (ratio between the combustion heat of the ammonia decomposition products and ammonia) is about 1.16 for in the temperature range above 500°C.
Publisher:
Oxford: Elsevier Ltd
Language:
English
This feature requires javascript
This feature requires javascript
Back to results list
Previous
Result
4
Next
This feature requires javascript
This feature requires javascript
Searching Remote Databases, Please Wait
Searching for
in
scope:(USP_PRODUCAO),scope:(USP_EBOOKS),scope:("PRIMO"),scope:(USP),scope:(USP_EREVISTAS),scope:(USP_FISICO),primo_central_multiple_fe
Show me what you have so far
This feature requires javascript
This feature requires javascript